Performance and Modeling of Moving Bed Biofilm Process for Nutrient Removal from Wastewater

Document Type : Research Paper

Authors

1 Assist. Prof. of Environmental Health Eng., Faculty of Public Health, Iran University of Medical Sciences, Tehran

2 Prof. of Environmental Health Engineering, Faculty of Public Health, Isfahan University of Medical Sciences, Isfahan

3 Assist. Prof. of Environmental Health Eng., Faculty of Public Health, Isfahan University of Medical Sciences, Isfahan

Abstract

In this study, experiments have been conducted to evaluate the removal of nutrients from synthetic wastewater using a moving bed biofilm process. For this purpose, the process was applied in series with anaerobic, anoxic, and aerobic units in four separate reactors. Moving bed biofilm reactors were operated continuously at different loading rates of nitrogen and phosphorus and different hydraulic retention times. In addition, for kinetic analysis,first-order substrate removal, Grau, and Stover-Kincannon models were tested with the experimental data. Based on the results obtained, a close to complete nitrification with an average Total Kjeldahl Nitrogen (TKN) removal efficiency of 99.72% was obtained in the aerobic reactor under optimum conditions. In this reactor, the average specific nitrification rate was 1.92 g NOx-N/kg VSS.h. During the study, statistically significant correlation was observed between the aerobic phosphorus removal rate and the anaerobic phosphorus release rate. Under optimum conditions, the average total nitrogen and phosphorus removal efficiencies were 80.9% and 95.8%, respectively. Finally, based on the kinetic analysis and with regard to nitrogen and phosphorus removals, the Stover-Kincannon model was selected as suitable for analyzing the experimental data and modelling of the moving bed biofilm process.

Keywords


1- Gerardi, M.H. (2002). Nitrification and denitrification in the activated sludge process, John Wiley and Sons Inc., New York.
2- Bonomo, L., Pastorelli, G., Quinto, E., and Rinaldi, G. (2000). “Tertiary nitrification in pure oxygen moving bed biofilm reactors.” Water Science and Technology, 41 (4-5), 361-368.
 
آب و فاضلاب                                                                                                                                                                      شماره 3 سال 1389
 
 
3- Mohammad Yari, N., and Balador, A. (2008). “Performance of MBBR in the treatment of combined municipal and industrial wastewater, A case study: Mashhad sewage treatment plant of Parkandabad.” J. of Water and wastewater, 65, 38-46.
4- Dulkadiroglu, H., Cokgor, E.U., Artan, N., and Orhon, D. (2005). “The effect of temperature and sludge age on COD removal and nitrification in a moving bed sequencing batch biofilm reactor.” Water Science and Technology, 51 (11), 95-103.
5- Ødegaard, H. (2006). “Innovations in wastewater treatment: The moving bed biofilm process.” Water Science and Technology, 53 (9), 17-33.
6- Ødegaard, H., Rusten, B., and Siljudalen, J. (1999). “The development of the moving bed biofilm process-from idea to commercial product.” European Water Management, 2 (3), 36-43.
7- Pastorelli, G., Canziani, R., Pedrazzi, L., and Rozzi, A. (1999). “Phosphorus and nitrogen removal in moving-bed sequencing batch biofilm reactors.” Water Science and Technology, 40 (4-5), 169-176.
8- Rusten, B., Eikebrokk, B., Ulgenes, Y., and Lygren, E. (2006). “Design and operation of the kaldnes moving bed biofilm reactors.” Aquacultural Engineering, 34, 322-331.
9- Kishida, N., Kim, J., Tsuneda, S., and Sudo, R. (2006). “Anaerbic/oxic/anoxic granular sludge process as an effective nutrient removal process utilizing denitrifying polyphosphate-accumulating organisms.” Water Research, 40, 2303-2310.
10- APHA, AWWA, WEF. (1999). Standard methods for the examination of water and wastewater, 20th Ed., American Public Health Association, Washington DC.
11- Chuang, S.H., Ouyang, C.F., Yuang, H. C., and You, S.J. (1998). “Evaluation of phosphorus removal in anaerobic-anoxic-aerobic system-via polyhydroxyalkonoates measurements.” Water Science and Technology, 38 (1), 107-114.
12- Okunuki, S., Kawaharasaki, M., Tanaka, H., and Kanagawa, T. (2004). “Changes in phosphorus removing performance and bacterial community structure in an enhanced biological phosphorus removal reactor.” Water Research, 38 (9), 2432-2438.
13- Helness, H., and Ødegaard, H. (1999). “Biological phosphorus removal in a sequencing batch moving bed biofilm reactor.” Water Science and Technology, 40 (4-5), 161-168.
14- Borghei, S.M., Sharbatmaleki, M., Pourrezaei, P., and Borghei, G. (2008). “Kinetics of organic removal in fixed-bed aerobic biological reactor.” Bioresource Technology, 99, 1118-1124.
15- Sharbatmaleki, M. A., and Borghei, S. M. (2006). “Performance of pumice stone as a packing in fixed-bed aerobic bioreactor.” J. of Water and Wastewater, 56, 62-71.
16- Grau, P., Dohanyas, M., and Chudoba, J. (1975). “Kinetic of Multicomponent Substrate Removal by Activated Sludge.” Water Research, 9, (7) 637-642.
17- Delnavaz, M., Ayati, B., and Ganjidoust, H. (2009). “Treatment of wastewater containing Anilin using a moving bed biofilm reactor (MBBR).” J. of Water and Wastewater, 68, 9-18.
18- Delnavaz, M., Ayati, B., and Ganjidoust, H. (2009). “Reaction kinetics of aniline synthetic wastewater treatment by moving bed biofilm reactor.” J. of Health and Environment, 2 (1), 76-87.
19- Kincannon Don, F., and Stover Enos, L. (1982). “Design methodology for fixed film reactor- RBC>s and biological towers.” J. Civil Eng for Practicing and Design Eng., 2,107-124.
20- Hosseiny, S. H., and Borghei, S. M. (2002). “Modelling of organic removal in a moving bed biofilm reactor (MBBR).” Scientia Iranica, 9 (1), 53-58.
21- Hooshyari, B., Azimi, A., and Mehrdadi, N. (2009). “Kinetic analysis of enhanced biological phosphorus removal in a hybrid integrated fixed film activated sludge process.” International J. of Environmental Sciences and Technology, 6 (1), 149-158.
22- Kavoosi, A., and Borgheei, S. M. (2005). “The use of light expanded clay aggregates as a biological support in wastewater treatment.” J. of Water and Wastewater, 53, 37-47.